BR112012032686B1 - composition - Google Patents

Abstract

COMPOSITION The embodiments of the invention provide crystalline block composites and their use as compatibilizers.

Description

Field of invention

[0001] The present invention relates to crystalline block composites and their use as polymer compatibilizers. History of the invention

[0002] Multiphase polymer blends are of great economic importance in the polymer industry. In general, commercial polymer blends consist of two or more polymers. In some cases, they can be combined with small amounts of a compatibilizer or interfacial agent.

[0003] Traditional and chemically unmodified polypropylenes have limited processability in applications that require melt strength. Without sufficient melt strength, polypropylene exhibits limited capacity in conversion processes, such as blow molding of large parts, thermoforming, extrusion coating, and some blown film applications. Chemically cross-linked or coupled polypropylenes can resolve some of these limitations, although cross-linked polymers generally have more deficient mechanical properties (eg, low extensibility). The additional cost of various crosslinking technologies, such as azide modification or electron beam application, can be prohibitive. It would be highly desirable to improve the melt strength of polypropylene by making it compatible with other polyolefins that have higher melt strength, such as polyethylene containing high levels of long chain branching, such as Low Density Polyethylene (LDPE). However, polypropylene blends and most polyethylenes are incompatible and result in immiscible blends with unsatisfactory mechanical and optical properties.

[0004] Block copolymers can be used as compatibilizers. Block copolymers comprise sequences ("blocks") of the same monomer unit, covalently linked to sequences of a different type. The blocks can be connected in a variety of ways, A-B in diblock structures and A-B-A in triblock structures, where A represents one block and B represents a different block. In a multi-block copolymer, A and B can be connected in several different ways and be repeated in multiple ways. The block copolymer may also comprise additional blocks of a different type. Multiblock copolymers can be linear multiblock polymers, star multiblock polymers (in which all the blocks bond to the same atom or chemical portion) or "comb" polymers, where the B blocks are attached, in one end, to an A main chain.

[0005] A block copolymer is created when two or more polymer molecules of different chemical composition are covalently linked together. Although a wide variety of block polymer architectures are possible, several block copolymers involve the covalent bonding of hard plastic blocks, which are substantially crystalline or glassy, to elastomeric blocks forming thermoplastic elastomers. Other block copolymers, such as rubber-rubber (elastomer-elastomer), glass-glass and crystalline glass-block block copolymers are also possible.

[0006] One method for preparing block copolymers is to produce a "live polymer". Unlike typical Ziegler-Natta polymerization processes, live polymerization processes involve only the initiation and propagation steps and essentially do not contain side chain termination reactions. This allows for the synthesis of predetermined and well-controlled structures desirable in a block copolymer. A polymer created in a "living" system can have a narrow or extremely narrow molecular weight distribution and be essentially monodispersed (that is, the polydispersity index (PDI) is essentially unique). Living catalytic systems are characterized by a rate of initiation on the order of or exceeding the rate of propagation, and by the absence of termination or transfer reactions. In addition, these catalytic systems are characterized by the presence of a simple type of active site. To produce a high block copolymer yield in a polymerization process, these catalysts must exhibit living characteristics to a substantial degree.

[0007] Another method for producing block copolymers involves the use of chain transfer technology. Such methods are exemplified, for example, in WO2005 / 090425, WO2005 / 090426, WO2005 / 090427 and WO2007 / 035489. In chain transfer, block copolymers can be produced by translating a growing polymer chain between two or more catalysts in a given reactor environment, and through this method each catalyst produces a different type of polymer. Catalysts can produce polymers that differ in the amount or type of comonomer incorporated in them, the density, the amount of crystallinity, the size of the crystallite attributable to a polymer of such composition, the type or degree of tacticity (isotactic or syndiotactic), regioregularity or regioirregularity, the amount of branching, including long chain branching or hyper-branching, homogeneity, or any other chemical or physical property. The transfer mechanism employs one or more transfer agents, which do not produce polymers, but which serve to transfer the polymer between active catalytic sites. Alternatively, the chain transfer can be used to produce a block copolymer using two or more reactors in series. In this case, the transfer agent acts to prolong the average life of a growing polymeric chain, so that the polymeric chains experience growth in each reactor before termination. The composition of each of the polymeric blocks is determined by the catalyst (s) and the reaction conditions.

Summary of the invention

[0008] Compositions are described comprising: a) a crystalline polyalphaolefin, polypropylene or a crystalline propylene copolymer; b) a low density polyethylene, and c) at least one crystalline block composite, comprising: i) a crystalline ethylene-based polymer 11) a crystalline alpha-olefin-based polymer and iii) a block copolymer comprising a block crystalline ethylene and a block of crystalline alpha-olefin.

Brief description of the drawings

[0009] Figure 1 shows a general graphical representation of the ratio of fraction by weight of CAO in the polymer to CBCI;

[0010] Figure 2 shows DSC curves for CBC1;

[0011] Figure 3 shows the FTREF analysis of CBC1;

[0012] Figure 4 shows HTLC analysis of CBC1;

[0013] Figure 5 shows a TEM micrograph of CBC1 at 2 μm resolution;

[0014] Figure 6 shows a TEM micrograph of CBC1 at 0.5 μm resolution;

[0015] Figure 7 shows a TEM micrograph of CBC1 at 100 nm resolution;

[0016] Figure 8 shows an TEM micrograph of Mix B compared to Mix 4 at 1 μm resolution;

[0017] Figure 9 shows the Melt Strength Comparison of Mixtures 1 and 3 containing 10% by weight of LDPE1 and compatible with CBC1 with Mixture A containing 10% by weight of LDPE1;

[0018] Figure 10 shows the Melt Strength Comparison of Mixtures 2 and 4 containing 20% by weight of LDPE1 and made compatible with CBC1 with Mixture B containing 20% by weight of LDPE1;

[0019] Figure 11 shows the Extensional Viscosity Comparison of PP / LDPE mixtures compatible with CBC1 with a polypropylene, a PP, LDPE mixture and a type of LDPE;

[0020] Figure 12 shows the Melt Strength Comparison of Mixtures 4, 6 and 7 containing 20-67.5% by weight of LDPE1 and compatible with CBC1 with Mixture B containing 20% by weight of LDPE1;

[0021] Figure 13 shows the Melt Strength Comparison of Mixtures 8 and 10 containing 20-45% by weight of LDPE1 and compatible with CBC1 with Mixture C containing 25% by weight of LDPE1; and

[0022] Figure 14 Comparison of Melt Strength of Mixtures 9 and 11 containing 20-45% by weight of LDPE1 and compatible with CBC1 with Mixture D containing 25% by weight of LDPE1.

Description of embodiments of the invention

[0023] All references to the Periodic Table of Elements in the present invention refer to the Periodic Table of Elements published and protected by copyright by CRC Press, Inc., 2003. Likewise, any references to a Group or Groups refer to to the Group or Groups in the aforementioned Periodic Table of Elements

[0024] Using the IUPAC system to enumerate groups. Unless otherwise stated, implicit in context, or common in the prior art, all parts and percentages are based on weight. For the purposes of American patent practice, the contents of any patent, patent application, or publication cited herein are hereby incorporated by reference in their entirety (or the equivalent American version thereof so incorporated by reference), especially with respect to the description of synthetic techniques, definitions (provided they do not contradict any definition provided here) and general knowledge of the state of the art.

[0025] The term "comprising" and its derivatives, is not intended to exclude the presence of any additional component, step or procedure, whether or not they are described in the present invention. For the avoidance of doubt, all compositions claimed herein using the term "comprising" may include any additive, adjuvant or additional compound, whether polymeric or otherwise, unless stated otherwise. On the contrary, the term "essentially consisting of" excludes any other component, step or procedure from the scope of any subsequent quotation, with the exception of those not essential to operability. The term "consisting of", excludes any component, step or procedure not specifically described or listed. The term "or", unless otherwise stated, refers to the related members individually, as well as in any combination.

[0026] The term "polymer" includes both conventional homopolymers, that is, homogeneous polymers prepared with a single monomer, and copolymers (alternatively referred to herein as interpolymers), meaning polymers prepared by reacting at least two monomers or otherwise containing segments or blocks chemically differentiated in them, even if formed with a simple monomer.

[0027] More specifically, the term "polyethylene" includes ethylene homopolymers and ethylene copolymers and one or more C3-8 α-olefins in which ethylene comprises at least 50 mole percent.

[0028] The term "polypropylene" includes propylene homopolymers, such as isotactic polypropylene, syndiotactic polypropylene, and propylene copolymers and one or more C2,4-8 α-olefins, in which propylene comprises at least 50 mole percent. Preferably, a plurality of polymerized monomer units of at least one block or segment in the polymer (a crystalline block) comprises propylene, preferably at least 90 mole percent, more preferably at least 93 mole percent and most preferably at least 95 mole Percent. A polymer prepared primarily with a different α-olefin, such as 4-methyl-1-pentene, should be similarly named.

[0029] The term "crystalline", if used, refers to a polymer or polymer block that has a first order transition or crystalline melting point (Tm) as determined by differential scanning calorimetry (DSC) or equivalent technique. The term can be used interchangeably with the term "semi-crystalline".

[0030] The term "crystallizable" refers to a monomer that can polymerize so that the resulting polymer is crystalline. Crystalline ethylene polymers typically have, although they are not restricted to densities from 0.89 g / cm3 to 0.97 g / cm3 and melting points of 75 ° C to 140 ° C. Crystalline propylene polymers typically have, although they are not restricted to densities from 0.88 g / cm3 to 0.91 g / cm3 and melting points from 100 ° C to 170 ° C.

[0031] The term "amorphous" refers to a polymer without a crystalline melting point.

[0032] The term "isotactic" is defined as polymer repeating units having at least 70 percent isotactic pennants, as determined through 13C-NMR analysis. "Highly isotactic" is defined as polymers having at least 90 percent isotactic pennants.

[0033] The term "block copolymer" or "segmented copolymer" refers to a polymer comprising two or more chemically distinct regions or segments (called "blocks") joined in a linear fashion, that is, a polymer comprising chemically differentiated units which are joined (covalently linked) from end to end in relation to the polymerized functionality, rather than in pendant or grafted form. In a preferred embodiment, the blocks differ in the amount or type of comonomer incorporated in them, density, amount of crystallinity, type of crystallinity (eg polyethylene versus polypropylene), size of the crystallite attributable to a polymer of such composition, type or degree of tacticity (isotactic or syndiotatic), regioregularity or regioirregularity, amount of branching, including long chain or hyper-branching branching, homogeneity or any other chemical or physical property. The block copolymers of the invention are characterized by unprecedented distributions of both the polydispersity of the polymer (PDI or Mw / Mn) and the block extension distribution, due, in a preferred embodiment, to the effect of the transfer agent (s) in combination with the catalyst (s).

[0034] The term "crystalline block composite" (CBC) refers to new polymers of the invention comprising a crystalline ethylene-based polymer (CEP), a crystalline alpha-olefin-based polymer (CAOP), and a copolymer block having a crystalline ethylene block (CEB) and a crystalline alpha-olefin block (CAOB), the CEB of the block copolymer having essentially the same composition as the CEP in the block composite and the CAOB of the block copolymer having essentially the same composition as the CAOP of the block composite. Additionally, the compositional division between the quantity of CEP and CAOP will be essentially the same as that between the corresponding blocks in the block copolymer. Block copolymers can be linear or branched. More specifically, each of the respective block segments contains long chain branches, although the block copolymer segment is substantially linear rather than containing grafted or branched blocks. When produced in a continuous process, crystalline block composites desirably have PDI of 1.7 to 1.5, preferably 1.8 to 10, preferably 1.8 to 5, more preferably 1.8 to 3.5.

[0035] CAOB refers to highly crystalline blocks of polymerized alpha-olefin units in which the monomer is present in an amount greater than 90 mole percent, preferably greater than 93 mole percent, more preferably greater than 95 mole percent , and preferably greater than 96 mole percent. In other words, the comonomer content in the CAOBs is less than 10 mole percent, and preferably less than 7 mole percent, and more preferably less than 5 mole percent, and most preferably less than 4 mole percent. Propylene crystallinity CAOBs have corresponding melting points of 80 ° C and above, preferably 100 ° C and above, more preferably 115 ° C and above, and most preferably 120 ° C and above. In some embodiments, CAOB comprises all or substantially all of the propylene units. CEB, on the other hand, refers to blocks of polymerized ethylene units in which the comonomer content is 10 mole percent or less, preferably between 0 mole percent and 10 mole percent, more preferably between 0 mole percent and 7 mole percent and most preferably between 0 mole percent and 5 mole percent. Such CEBs have melting points preferably at 75 ° C and above, more preferably at 90 ° C and 100 ° C and above. Polymerization Methods

[0036] The crystalline block composite polymers of the invention are preferably prepared by a process comprising contacting a monomer or mixture of monomers polymerizable by addition under conditions of polymerization by addition with a composition comprising at least one polymerization catalyst by addition, one cocatalyst and a chain transfer agent, said process being defined by the formation of at least part of the growing polymer chains under different process conditions in two or more reactors operating under constant state polymerization conditions or in two or more zones of polymerization a reactor operating under piston flow polymerization conditions.

[0037] Suitable processes of this type and useful for producing the crystalline block composites of the invention can be found, for example, in American patent application publication No. 2008/0269412, published on October 30, 2008, incorporated herein by reference . Particularly, the polymerization is desirably conducted as continuous polymerization, preferably a continuous polymerization in solution, where the catalytic components, monomers and optionally solvent, sweepers and polymerization aids are continuously supplied to one or more reactors or zones, and the polymer product is continuously removed of the same. In the scope of the terms "continuous" and "continuously", as used in this context, they refer to those processes in which there are intermittent additions of reagents and the removal of products in small regular and irregular intervals, so that, over time, all the process is substantially continuous. In addition, as previously explained, the chain transfer agent (s) can be added at any point during polymerization, including in the first reactor or zone, at the outlet or just before the outlet of the first reactor, or between the first reactor or zone and the second or any reactor or back zone. Due to the difference in monomers, temperatures, pressures or other difference found in the polymerization conditions between at least two of the reactors or zones connected in series, the polymeric segments of different composition, such as comonomer content, crystallinity, density, tactility, regioregularity or another chemical or physical difference, in the same molecule are formed in different reactors or zones. The size of each segment or block is determined by continuous polymer reaction conditions, the most likely distribution being the polymer size.

[0038] Each reactor in the series can be operated under polymerization conditions under high pressure, in solution, in paste, or in gas phase. In a multiple zone polymerization, all zones operate under the same type of polymerization, such as in solution, paste or gas phase, but under different process conditions. For a solution polymerization process, it is desirable to use homogeneous dispersions of the catalytic components in a liquid diluent in which the polymer is soluble under the polymerization conditions employed. Such a process using an extremely fine silica or similar dispersing agent to produce such a homogeneous catalyst dispersion, in which normally the metal complex or cocatalyst is poorly soluble, is described in US-A-5,783,512. A high pressure process is generally conducted at temperatures of 100 ° C to 400 ° C and under pressures greater than 500 bar (50 MPa). A paste process typically uses an inert hydrocarbon diluent and temperatures ranging from 0 ° C to a temperature just below the temperature at which the resulting polymer becomes substantially soluble in the inert polymerization medium. Preferred temperatures in a paste polymerization are 30 ° C, preferably 60 ° C to 115 ° C, preferably up to 100 ° C. Pressures typically range from atmospheric (100 kPa) to 3.4 MPa (500 psi).

[0039] In all the aforementioned processes, conditions of continuous or substantially continuous polymerization are preferably employed. The use of such polymerization conditions, especially processes of continuous polymerization in solution, allows the use of high reactor temperatures, which results in the economical production of the crystalline block composites of the present invention with high yields and efficiencies. Solution processes are particularly advantageous since the catalysts and chain transfer agents are free to mix and react, allowing polymer chain transfer reactions easier than those that occur, for example, in polymerization reactors in paste or in gas phase.

[0040] The catalyst can be prepared in the form of a homogeneous composition by adding the metal complex or multiple complexes necessary for a solvent in which the polymerization will be conducted or in a diluent compatible with the final reaction mixture. The desired cocatalyst or activator and, optionally, the transfer agent, can be combined with the catalyst composition either before, simultaneously with or after combining the catalyst with the monomers to be polymerized and any additional reaction diluent.

[0041] During the entire period, the individual ingredients, as well as any active catalyst composition, must be protected from oxygen, moisture and other catalytic poisons. Therefore, the catalyst components, transfer agent and activated catalysts must be prepared and stored in an atmosphere free of oxygen and moisture, preferably under dry inert gas, such as nitrogen.

[0042] Without restricting the scope of the invention in any way, one of the means for conducting such a polymerization process is described below. In one or more agitated tank or loop reactors operating under solution polymerization conditions, the monomers to be polymerized are introduced continuously together with any solvent or diluent in a part of the reactor. The reactor contains a relatively homogeneous liquid phase composed substantially of monomers together with any solvent or diluent and dissolved polymer. Preferred solvents include C4-10 hydrocarbons or mixtures thereof, especially alkanes, such as hexane or mixtures of alkanes, as well as one or more of the monomers employed in the polymerization. Examples of suitable loop reactors and a variety of suitable operating conditions for use with them, including the use of multiple loop reactors, operating in series, are found in USPs patents 5,977,251, 6,319,989 and 6,683,149.

[0043] The catalyst together with the cocatalyst and, optionally, the chain transfer agent, are continuously or intermittently introduced into the liquid phase of the reactor or any recycled portion of it, at least from a single location. The reactor temperature and pressure can be controlled by adjusting the solvent / monomer ratio, the catalyst addition rate, as well as using cooling or heating coils, liners or both. The rate of polymerization is controlled by the rate of addition of catalyst. The content of a given monomer in the polymeric product is influenced by the ratio of monomers in the reactor, which is controlled by manipulating the respective feed rates of these components to the reactor. The molecular weight of the polymeric product is optionally controlled by controlling other polymerization variables, such as temperature, monomer concentration, or by the previously mentioned chain transfer agent, or a chain terminating agent, such as hydrogen, such as it is known in the state of the art. Connected to the reactor discharge, optionally by means of a conduit or other transfer medium, there is a second reactor so that a large portion of the polymeric chains is inert through connection to the chain transfer agent and has the potential to grow further more in the second reactor. Between the first and second reactors, a differential in at least one process condition is established. Preferably, for use in forming a copolymer of two or more monomers, the difference is the presence or absence of one or more comonomers or a difference in the comonomer concentration. Additional reactors, each arranged similarly to the second reactor in the series, can also be provided. Upon leaving the last reactor in the series, the effluent is contacted with a catalyst poison agent such as water, steam or an alcohol or with a coupling agent.

[0044] When producing a block polymer with a crystalline ethylene block (CEB) and a crystalline alpha-olefin block (CAOB) in two reactors or zones, it is possible to produce CEB in the first reactor or zone and CAOB in the second reactor or zone or produce the CAOB in the first reactor or zone and the CEB in the second reactor or zone. It is more advantageous to produce CEB in the first reactor or zone with fresh chain transfer agent added. The presence of increased levels of ethylene in the reactor or zone producing CEB will typically lead to a much higher molecular weight in that reactor or zone than in the zone or reactor producing CAOB. The fresh chain transfer agent will reduce the MW of the polymer in the reactor or in the zone that is producing CEB, thus leading to a better total balance between the extension of the CEB and the CAOB segments.

[0045] When operating reactors or zones in series, it is necessary to maintain different reaction conditions so that one reactor produces CEB and the other CAOB. The transfer of ethylene from the first reactor to the second reactor (in series) or from the second reactor back to the first reactor through a solvent and monomer recycling system is preferably minimized. There are many possible unit operations to remove this ethylene, however, because ethylene is more volatile than higher alpha-olefins, a simple way is to remove most unreacted ethylene through a quick step, reducing the pressure of effluent from the reactor that produces CEB and evaporating ethylene. A more preferable method is to avoid additional unit operations and use the much greater reactivity of ethylene versus higher alpha-olefins, so that the conversion of ethylene in the CEB reactor approaches 100%. The overall conversion of monomers in the reactors can be controlled by maintaining the conversion of alpha-olefin at a high level (90 to 95%).

[0046] The resulting polymeric product can be recovered by evaporating the volatile components of the reaction mixture, such as residual monomers or diluent under reduced pressure, and, if necessary, conducting further devolatilization in equipment, such as a devolatilization extruder. In a continuous process, the average residence time of the catalyst and polymer in the reactor is generally 5 minutes to 8 hours, and preferably 10 minutes to 6 hours.

[0047] Alternatively, the aforementioned polymerization can be carried out in a flow reactor pistoned with a monomer, catalyst, transfer agent, temperature or other gradient established between different zones or regions of the same, optionally accompanied by separate addition of catalysts and / or chain transfer agent, and operating under adiabatic or non-adiabatic polymerization conditions. The catalyst, monomers, or transfer agent can be introduced only at the beginning of the piston flow reactor or at various points throughout the reactor extension.

[0048] The catalyst composition can also be prepared and used as a heterogeneous catalyst by adsorbing the necessary components on an inorganic or inert organic particulate solid, as previously described. In a preferred embodiment, a heterogeneous catalyst is prepared by co-precipitating the metal complex and the reaction product of an inert inorganic compound and an activator containing active hydrogen, especially the reaction product of a tri (C1-4alkyl) aluminum compound and a salt of an ammonium hydroxyaryltris (pentafluorophenyl) borate, such as ammonium (4-hydroxy-3,5-diterciaributylphenyl) tris (pentafluorophenyl) borate salt. When prepared in heterogeneous or supported form, the catalyst composition can be used in a paste or gas phase polymerization. As a practical limitation, paste polymerization occurs in liquid diluents in which the polymeric product is substantially insoluble. Preferably, the diluent for slurry polymerization is one or more hydrocarbons with less than 5 carbon atoms. If desired, saturated hydrocarbons such as ethane, propane or butane can be used, in whole or in part, as a diluent. With a solution polymerization, the α-olefin comonomer or a mixture of different α-olefin monomers can be used, in whole or in part, as a diluent. Most preferably, at least an important part of the diluent comprises the α-olefin monomer or monomers to be polymerized (s).

[0049] In a preferred embodiment, the crystalline block composites of the invention comprise a fraction of block polymer that has the most likely distribution of block extensions. Preferred block polymers according to the invention are block copolymers containing 2 or 3 blocks or segments. In a polymer containing three or more segments (that is, blocks separated by a distinguishable block), each block can be the same or chemically different and generally defined by a distribution of properties. In a process to prepare polymers, chain transfer is used as a way to extend the life of a polymer chain, so that a substantial fraction of the polymer chains egress from at least the first reactor in a series of multiple reactors, or of the first reactor zone in a multizone reactor, operating substantially under piston flow conditions in the form of polymer terminated with a chain transfer agent. When transferring a polymer chain from the chain transfer agent back to a catalyst, in a reactor or back zone, the growth of the polymer chain occurs under different polymerization conditions. Different polymerization conditions in the respective reactors or zones include the use of different monomers, comonomers, or different monomer / comonomer (s) ratio, different polymerization temperatures, different pressures or partial pressures of several monomers, different catalysts, different monomer gradients, or any other difference that leads to the formation of a distinguishable polymeric segment. Thus, at least a portion of the polymer comprises two, three or more, preferably two or three differentiated polymeric segments, arranged in a linear sequence.

[0050] The next mathematical treatment of the resulting polymers is based on theoretically derived parameters which, it is believed, apply and demonstrate that, especially in two or more reactors or continuous zones and in constant state connected in series, with different conditions of polymerization to which the growing polymer is exposed, the block extensions of the polymer that are formed in each reactor or zone, adjust to a more likely distribution, derived as follows, where pi is the probability of propagation of the polymer in a reactor, with respect to catalyst block sequences i. The theoretical treatment is based on standard hypotheses and methods known in the prior art and used to predict the effects of polymerization kinetics on molecular architecture, including the use of mass reaction action rate expressions that are not affected by extensions of chain or block, and in the hypothesis that the growth of the polymeric chain is completed in a very short time compared to the average residence time of the reactor. These methods were previously described in W.H. Ray, J. Macromol. Sci., Rev. Macromol. Chem. C8, 1 (1972) and A. E. Hamielec and J.F.MacGregor, "Polymer Reaction Engineering", K.H. Reichert and W.Geisler, Eds. Hanser, Munich, 1983. In addition, it is assumed that each incidence of the chain transfer reaction in a given reactor results in the formation of a simple polymeric block, while the transfer of the chain transfer agent terminated polymer to a different reactor or zone and exposure to different polymerization conditions results in the formation of a different block. For catalyst i, the fraction of n extension sequences being produced in a reactor is given by Xi [n], where n is an integer from 1 to infinity, representing the total number of monomer units in the block. Xi [n] = (1-pi) pi (n-1) the most likely distribution of block extensions Ni = 1/1-pi average numerical extension of blocks

para cada catalisador i = {1,2...], onde Rp[i] = taxa local de consumo de monômero por catalisador i (moles/L/tempo), Rt[i] = taxa total de transferência e terminação de cadeia para catalisador i (moles/L/tempo), e Rs[i] = taxa local de traslado de cadeia com polímero inerte (moles/L/tempo).[0051] If more than one catalyst is present in a reactor or zone, each catalyst will have the probability of propagation (pi) and, therefore, will present an unprecedented average block length, with the polymer distribution being made in that reactor or zone . In a more preferred embodiment, the probability of propagation is defined as follows:

for each catalyst i = {1,2 ...], where Rp [i] = local rate of monomer consumption per catalyst i (moles / L / time), Rt [i] = total transfer rate and chain termination for catalyst i (moles / L / time), and Rs [i] = local rate of chain transfer with inert polymer (moles / L / time).

[0052] For a given reactor, the polymer propagation rate, Rp [i] is defined using an apparent rate constant kpi, multiplied by a total monomer concentration, [M [and multiplied by the local catalyst concentration i , [Ci], as follows: Rp [i] = kpi [M] [Ci]

[0053] Chain transfer, termination, and transfer rate, is determined as a function of chain transfer to hydrogen (H2), beta hydride elimination, and chain transfer to chain transfer agent (CSA). The quantities [H2] and [CSA] are molar concentrations and each subscribed k value is a constant rate for the reactor or zone: Rt [i] = kH2i [H2] [Ci] + kβi [Ci] + kai [CSA] [ Ci]

[0054] Inert polymer chains are created when a polymer portion is transferred to a CSA and it is assumed that all reacting CSA portions are each paired with an inert polymer chain. The rate of transfer of inert polymer chain with catalyst i is given as follows, where [CSAf] is the feed concentration of CSA, and the amount ([CSAf] - [CSA]) represents the concentration of inert polymer chains: Rs [i] = kai [Ci] ([CSAf] - [(CSA])

[0055] As a result of the aforementioned theoretical treatment, it can be observed that the global block extension distribution for each resulting block copolymer block is a sum of the block extension distribution given previously by Xi [n], weighted by rate of local polymer production for catalyst i. This means that a polymer prepared under at least two different polymer forming conditions will have at least two distinguishable blocks or segments, each having a more likely block extension distribution.

Monomers

[0056] Monomers suitable for use in the preparation of crystalline block composites of the present invention include ethylene, propylene, or any other olefin that produces a crystalline polymer, and any polymerisation comonomer by addition. The polymerizable comonomers are preferably any olefin or diolefin comonomer, more preferably any α-olefin comonomer. Examples of suitable comonomers include 2 to 30 straight-chain or branched α-olefins, preferably 2 to 20 carbon atoms, such as ethylene, propylene, 1-butene, 1-pentene, 3-methyl-1-butene, 1 -hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosene, cyclo-olefins from 3 to 30, preferably from 3 to 20 carbon atoms, such as cyclopentene, cycloheptene, norbornene, 5-methyl-2-norbornene, tetracyclododecene, and 2-methyl-1,4,5,8-dimethane-1,2 , 3,4,4a, 5,8,8a-octahydronaphthalene; di and polyolefins, such as butadiene, isoprene, 4-methyl-1,3-pentadiene, 1,3-pentadiene, 1,4-pentadiene, 1,5-hexadiene, 1,4-hexadiene, 1,3-hexadiene, 1,3-octadiene, 1,4-octadiene, 1,5-octadiene, 1,6-octadiene, 1,7-octadiene, ethylidenonorbornene, norbornene vinyl, dicyclopentadiene, 7-methyl-1,6-octadiene, 4-ethylidene -8-methyl-1,7-nonadiene, and 5,9-dimethyl-1,4,8-decatriene; aromatic vinyl compounds such as mono- or polyalkylstyrenes (including styrene, o-methyl styrene, m-methyl styrene, p-methyl styrene, o, p-dimethyl styrene, o-ethyl styrene, m-ethyl styrene and p-ethyl styrene), and derivatives containing a functional group, such as methoxystyrene, ethoxystyrene, vinylbenzoic acid, methyl vinylbenzoate, vinylbenzyl acetate, hydroxystyrene, o-chloro-styrene, p-chloro-styrene, divinyl-benzene, 3-phenylpropene, 4-phenylpropene, and α-methylstyrene, vinyl chloride, 1,2 difluoroethylene, 1,2-dichlorethylene, tetrafluoroethylene, and 3,3,3-trifluoro-1-propene, as long as the monomer is polymerizable under the conditions employed.

Preferred monomers or mixtures of monomers for use in combination with at least one CSA in the present invention include ethylene; propylene; mixtures of ethylene with one or more monomers selected from the group consisting of propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, and styrene; and mixtures of ethylene, propylene and a conjugated or unconjugated diene.

Chain Transfer Agents and Catalysts

[0058] Catalysts and catalytic precursors suitable for use in the present invention include metal complexes, such as those described in WO2005 / 090426, in particular, those described at the beginning of page 20, line 30 through page 53, line 20, incorporated herein by reference. Suitable catalysts are also described in US 2006/0199930; US 2007/0167578; US 2008/0311812; US 7,355,089 B2; or WO 2009/012215 which are incorporated herein by reference with respect to catalysts.

onde: R20é um grupo aromático ou aromático inertemente substituído contendo de 5 a 20 átomos não contando hidrogênio, ou um derivado polivalente do mesmo; T3é um grupo hidrocarbileno ou silano tendo de 1 a 20 átomos não contando hidrogênio, ou um derivado inertemente substituído do mesmo; M3é um metal do Grupo 4, preferivelmente zircônio ou háfnio; G é um grupo ligante aniônico, neutro ou dianiônico; preferivelmente um grupo haleto, hidrocarbila ou diidrocarbilamida tendo até 20 átomos não contando hidrogênio;[0059] Particularly preferred catalysts are those with the following formula:

where: R20is an inertly substituted aromatic or aromatic group containing 5 to 20 atoms not containing hydrogen, or a polyvalent derivative thereof; T3is a hydrocarbilene or silane group having 1 to 20 atoms not containing hydrogen, or an inertly substituted derivative thereof; M3 is a Group 4 metal, preferably zirconium or hafnium; G is an anionic, neutral or dianionic linking group; preferably a halide, hydrocarbyl or dihydrocarbilamide group having up to 20 atoms not containing hydrogen;

[0060] g is a number from 1 to 5 indicating the number of such groups G; and electron donor bonds and interactions are represented by lines and arrows, respectively.

onde: T3é um grupo divalente em ponte de 2 a 20 átomos não contando hidrogênio, preferivelmente um grupo alquileno C3-6 substituído ou não substituído; e Ar2independentemente em cada ocorrência é um arileno ou um grupo arileno substituído com alquila ou arila com 6 a 20 átomos, não contando hidrogênio; M3é um metal do Grupo 4, preferivelmente háfnio ou zircônio; G independentemente em cada ocorrência é um grupo ligante aniônico, neutro ou dianiônico; g é um número de 1 a 5 indicando o número de tais grupos X; e as interações doadoras de elétron são representadas por setas.[0061] Preferably, such complexes correspond to the formula:

where: T3 is a divalent bridged group of 2 to 20 atoms not containing hydrogen, preferably a substituted or unsubstituted C3-6 alkylene group; and Ar2 independently at each occurrence is an arylene or an arylene group substituted with alkyl or aryl with 6 to 20 atoms, not counting hydrogen; M3 is a Group 4 metal, preferably hafnium or zirconium; G independently in each occurrence is an anionic, neutral or dianionic linking group; g is a number from 1 to 5 indicating the number of such groups X; and electron donor interactions are represented by arrows.

onde M3é Hf ou Zr; Ar4é arila C6-20 ou seus derivados inertemente substituídos, especialmente 3,5-di(isopropil)fenila, 3,5- di(isobutil)fenila, dibenzo-1H-pirrol-1-il ou antracen-5-ila, e T4independentemente em cada ocorrência compreende um grupo alquileno C3-6, um grupo cicloalquileno C3-6, ou um derivado inertemente substituído dos mesmos; R21independentemente em cada ocorrência é hidrogênio, halo, hidrocarbila, triidrocarbilsilila, ou triidrocarbilsililidrocarbila de até 50 átomos não contando hidrogênio; e G, independentemente em cada ocorrência, é um grupo halo ou um hidrocarbila ou triidrocarbilsilila de até 20 átomos não contando hidrogênio, ou 2 grupos G juntos são um derivado divalente dos grupos hidrocarbila ou triidrocarbilsilila anteriormente citados.[0062] Preferred examples of metal complexes of the aforementioned formula include the following compounds:

where M3 is Hf or Zr; Ar4 is C6-20 aryl or its inertly substituted derivatives, especially 3,5-di (isopropyl) phenyl, 3,5-di (isobutyl) phenyl, dibenzo-1H-pyrrol-1-yl or anthracen-5-yl, and T4 independently at each occurrence it comprises a C3-6 alkylene group, a C3-6 cycloalkylene group, or an inertly substituted derivative thereof; R21 independently in each occurrence is hydrogen, halo, hydrocarbyl, triidrocarbilsilila, or triidrocarbilsililidrocarbila of up to 50 atoms not counting hydrogen; and G, independently at each occurrence, is a halo group or a hydrocarbyl or trihydrocarbylsilyl of up to 20 atoms not counting hydrogen, or 2 G groups together are a divalent derivative of the hydrocarbyl or trihydrocarbylsilyl groups mentioned above.

onde Ar4é 3,5-di(isopropil)fenila, 3,5-di(isobutil)fenila, dibenzo-1H-pirrol-1-ila, ou antracen-5-ila, R21é hidrogênio, halo, ou alquila C1-4, especialmente metila, T4é propan-1,3-diila ou butan-1,4-diila, e G é cloro, metila ou benzila.[0063] Especially preferred are the compounds of the formula:

where Ar4is 3,5-di (isopropyl) phenyl, 3,5-di (isobutyl) phenyl, dibenzo-1H-pyrrol-1-yl, or anthracen-5-yl, R21is hydrogen, halo, or C1-4 alkyl, especially methyl, T4 is propan-1,3-diyl or butan-1,4-diyl, and G is chlorine, methyl or benzyl.

[0064] Other suitable metal complexes are those of the formula:

[0065] The polyvalent Lewis base complexes mentioned above are conveniently prepared through standard metallation and ligand exchange procedures involving a Group 4 metal source and the neutral polyfunctional ligand source. In addition, the complexes can also be prepared by means of an amide elimination and hydrocarbilization process, starting with the corresponding Group 4 metal tetraamide and a hydrocarbilizing agent, such as trimethylaluminum. Other techniques can also be used. These complexes are known in US patent reports US 6,320,005, 6,103,657, WO 02/38628, WO 03/40195 and US 04/0220050, among others.

[0066] Suitable cocatalysts are those described in WO2005 / 090426, in particular, those described on page 54, line 1 to page 60, line 12, incorporated herein by reference.

[0067] Suitable chain transfer agents are those described in WO2005 / 090426, in particular, those described on page 19, line 21 to page 20, line 12, incorporated herein by reference. Particularly preferred chain transfer agents are dialkyl zinc compounds.

[0068] Preferably, the block composite polymers of the invention comprise ethylene, propylene, 1-butene or 4-methyl-1-pentene, and optionally one or more comonomers in the polymerized form. Preferably, the block copolymers of the crystalline block composites comprise, in polymerized form, ethylene, propylene, 1-butene or 4-methyl-1-pentene and optionally one or more C4-20 α-olefin comonomers. Suitable optional comonomers are selected from diolefins, cyclic olefins, and cyclic diolefins, halogenated vinyl compounds, and aromatic vinylidene compounds.

[0069] The comonomer content in the resulting block composite copolymers can be measured using any suitable technique, with techniques based on preferred nuclear magnetic resonance (NMR) spectroscopy.

[0070] Preferably, the crystalline block composite polymers of the invention comprise from 0.5 to 95% by weight of CEP, from 0.5 to 95% by weight of CAOP and from 5 to 99% by weight of block copolymer . More preferably, the crystalline block composite polymers comprise from 0.5 to 79% by weight of CEP, from 0.5 to 79% by weight of CAOP, and from 20 to 99% by weight of block copolymer and more preferably from 0.5 to 49% by weight of CEP, from 0.5 to 49% by weight of CAOP and from 50 to 99% by weight of block copolymer. Weight percentages are based on the total weight of the crystalline block composite. The sum of the percentages by weight of CEP, CAOP and block copolymer is equal to 100%.

[0071] Preferably, the block copolymers of the invention comprise 5 to 95 weight percent crystalline ethylene (CEB) blocks and 95 to 5 weight percent crystalline alpha-olefin blocks (CAOB). They may comprise from 10% by weight to 90% by weight of CEB and from 90% by weight to 10% by weight of CAOB. More preferably, the block copolymers comprise from 25 to 75% by weight of CEB and from 75 to 25% by weight of CAOB, and even more preferably comprise from 30 to 70% by weight of CEB and from 70 to 30% by weight of CAOB.

[0072] The crystalline block composite polymers of the invention can be differentiated from conventional random copolymers, physical mixtures of polymers and block copolymers prepared via the addition of sequential monomer. Crystalline block composites can be differentiated from random copolymers and a physical mixture by characteristics such as crystalline block composite index, better tensile strength, improved fracture resistance, finer morphology, improved optics, and greater impact resistance to lowest temperature; of block copolymers prepared by sequential addition of monomer by molecular weight distribution, rheology, reduction in shear strength, rheology ratio, and because there is block polydispersity. Block segment polydispersity has been shown to be beneficial in the formation of fine dispersions of immiscible polymers. (R.B. Thompson and M.W. Matsen, Phys. Rev. Let., 2000, 85 (3), 670). An unprecedented feature of crystalline block composites is that they cannot be fractionated by conventional means by solvent or temperature, such as fractionation in xylene, solvent / non-solvent, or fractionation by elution and elevation of temperature or fractionation by elution and crystallization, since the individual blocks of the block copolymer are crystalline.

[0073] In some embodiments, the block composites of the invention have a Crystalline Block Composite Index (CBCI), as defined below, which is greater than zero, but less than about 0.4 or about 0.1 at about 0.3. In some embodiments, the CBCI is greater than about 0.4 and about up to 1.0. In some embodiments, CBCI is in the range of about 0.1 to about 0.9, about 0.1 to about 0.8, about 0.1 to about 0.7 or about from 0.1 to about 0.6. In addition, CBCI can be in the range of about 0.4 to about 0.7, about 0.5 to about 0.7, or about 0.6 to about 0.9. In some embodiments, the CBCI is in the range of about 0.3 to about 0.9, about 0.3 to about 0.8, or about 0.3 to about 0.7 of about from 0.3 to about 0.6, from about 0.3 to about 0.5, or from about 0.3 to about 0.4. In other embodiments, CBCI is in the range of about 0.4 to about 1.0, about 0.5 to about 1.0 or about 0.6 to about 1.0, about from 0.7 to about 1.0, from about 0.8 to about 1.0, or from about 0.9 to about 1.0.

[0074] Still preferably, the crystalline block composites of the present embodiment of the invention have a weight average molecular weight (Mw) from 1,000 to about 2,500,000, preferably from 35,000 to about 1,000,000 and more preferably from 50,000 to 500,000 , from 50,000 to about 300,000, and preferably from 50,000 to about 200,000.

[0075] The polymers of the invention can be extended in oil with from 5 to about 95 percent, preferably from 10 to 60 percent, more preferably from 20 to 50 percent, based on the total weight of the composition of an oil of processing. Suitable oils include any oil that is conventionally used in the manufacture of extended EPDM rubber formulations. Examples include both naphthenic and refined paraffinic oils, and amorphous low molecular weight synthetic polymerized polyalphaolefins, with paraffinic oils being preferred.

[0076] The polymers of the invention can be cross-linked with any appropriate cross-linking agent. Suitable crosslinking agents include, but are not limited to phenolic resin, peroxides, azides, aldehyde reaction products, vinyl silane grafted portions, hydrosilylation, substituted ureas, substituted guanidines; substituted xanthates; substituted dithiocarbamates; sulfur-containing compounds, such as thiazoles, imidazoles, sulfonamides, thiuramidisulfides, paraquinonodioxima, dibenzoparaquinonioxy, sulfur; and their combinations. Suitable crosslinking agents can also be used such as those described in U.S. Patent No. 7,579,408, col. 31, line 54 to column 34, line 52, the description of which is incorporated herein by reference.

[0077] Crosslinking can also be performed by applying radiation, such as with electronic beam radiation.

[0078] A composition according to the invention can include carbon black. Preferably, carbon black is present in the amount of 10 to 80 percent, more preferably 20 to 60 percent, based on the total weight of the composition.

[0079] Additional components of the formulations of the present invention advantageously employed in accordance with the present invention include various other ingredients in amounts that do not detract from the properties of the resulting composition. These ingredients include, but are not restricted to activators, such as calcium oxide or magnesium; fatty acids such as stearic acid and its salts; fillers and reinforcers, such as calcium or magnesium carbonate, silica, and aluminum silicates; plasticizers, such as dialkyl esters of dicarboxylic acids; anti-degraders; softeners; greases; and pigments.

[0080] HDPE / PP and Propylene based polymers suitable for Mixtures

[0081] Some embodiments of the present invention comprise compositions comprising 98 to 0.5% by weight of crystalline block composite with the remainder being polyethylene, polyalphaolefin and combinations thereof. Preferably, the compositions comprise 50 to 0.5% by weight of CBC and more preferably 15 to 0.5% by weight of CBC.

[0082] Any High Density Polyethylene (HDPE) or Linear Low Density Polyethylene (LLDPE) can be used as the polyethylene component, such as those produced via the gas phase process, in solution or paste with any of the chromium catalyst (Wide MWD), Ziegler-Natta catalyst (average MWD) or metallocene or post-metallocene catalyst (narrow MWD). In addition, any LDPE homopolymer or copolymer produced by free radical polymerization under high pressure in an autoclave or tubular reactor can be used. The polyethylene used in the present invention can be HDPE or LLDPE with densities from 0.90 to 0.98 g / cm3. In addition, polyethylene can be a low density polyethylene (LDPE) homopolymer with a density range of 0.91 to 0.94 g / cm3 or can be copolymerized with appropriate comonomers such as vinyl acetate, mono or dicarboxylic acids α , β-ethylenically unsaturated, and combinations thereof, glycidyl methacrylate, ethyl acrylate or butyl acrylate. LDPE copolymers containing α, β-ethylenically unsaturated mono- or dicarboxylic acids can be neutralized in a post-polymerization process with metal ions and compounds of alkali metals, alkaline earth metals, and transition metals; and their combinations. Specific cationic sources include, but are not restricted to, metal ions and compounds of lithium, sodium, potassium, magnesium, cesium, calcium, barium, manganese, copper, zinc, tin, rare earth metals, and combinations thereof. Any component or combination of polyethylene blend components can be used, provided that when mixed with a polypropylene or propylene elastomer or plastomer and at least one suitable block composite, they increase the melt strength of the blend composition with respect to the elastomer or polypropylene or propylene plastomer at least 10%, preferably 25%, and most preferably 50%.

[0083] Crystalline polyalphaolefin can be any polymer, such as polypropylene, polybutylene, poly (4-methylpentene), etc. A polypropylene polymer used in the present invention can be any polypropylene polymer prepared by any means known in the art, or a mixture of polypropylene polymer, such as a polypropylene homopolymer, a random ethylene or butene, polypropylene copolymer, or a mixture of impact-modified polypropylene containing a polypropylene homopolymer or a random crystalline copolymer of ethylene and propylene combined with a rubbery ethylene-propylene copolymer.

[0084] A propylene-based elastomer (PBE) or propylene-based plastomer (PBP) can also be used in the present invention, such as plastomers and elastomers VERSIFY (The Dow Chemical Company) and VISTAMAXX polymers (ExxonMobil Chemical Company) . A PBE or PBP can be used in amounts of 5 wt% to 95 wt%, preferably 10 wt% to 90 wt% and more preferably 30 wt% to 70 wt%.

[0085] The compositions of the invention provide improved properties compared to compositions of component A) and B) and without C). Particularly, the melt strength of the composition at 100 mm / s and 190 ° C, measured as detailed below, is at least 115% greater, preferably at least 120% greater, more preferably at least 130% greater and most preferably at least 140 % higher than the composition without C). In addition, the average particle size, measured as detailed below, of the composition is at least 50% smaller, preferably at least 60% smaller, more preferably at least 70% smaller and most preferably at least 80% smaller than that of composition without component C).

[0086] The compositions of the invention can be used in applications such as, but not limited to, blow molding of large parts, thermoforming, extrusion coating, and blown film applications, in addition to articles, molded parts and other applications. Test Methods

[0087] The total composition of each resin is determined using DSC, NMR, GPC, DMS and TEM morphology. HTLC fractionation is also used to assess the crystalline block composite index of the polymer, as explained below. The physical properties of polymers measured in polymers include tensile, optical, and melt elongation properties. Traction test

[0088] The stress-strain behavior in unaxial stress is measured using microtensile specimens according to ASTM D1708. The samples are stretched with an Instron at 50 mm / min at 23 ° C. Tensile strength and elongation at break are reported for an average of 5 specimens. Optical Properties

[0089] Opacity was measured according to ASTM D1003 using 0.5 mm compression molded films. Transparency was measured according to ASTM D1746 using 0.5 mm compression molded films. Polymer films are prepared by compression molding followed by rapid cooling. The polymer is pre-melted at 190 ° C for 1 minute at 6.9 MPa (1000 psi) and then compressed for 2 minutes at 34.5 MPa (5000 psi) and then quickly cooled between chilled plates (15-20 ° C ) for 2 minutes. Compression Molding Conditions

[0090] Polymer films and specimens (unless otherwise specified) are prepared by compression molding followed by rapid cooling using a Carver press (such as model # 4095-4PR1001R). The polymer is pre-melted at 190 ° C for 1 minute at 6.9 MPa (1000 psi) and then compressed for 2 minutes at 34.5 MPa (5000 psi) and then quickly cooled between chilled plates (15-20 ° C ) for 2 minutes.

Differential Scanning Calorimetry (DSC)

[0091] Differential Scanning Calorimetry is conducted on a TA Instruments DS1000 QC equipped with an RCS cooling accessory and an automatic sampler. A flow of nitrogen purge gas at 50 ml / min is used. The sample is pressed into a thin film and melted in the press at about 230 ° C and then cooled in air to room temperature (25 ° C). About 3-10 mg of material is then cut, weighed accurately, and placed in a light aluminum container (ca 50 mg) which is then closed by compression. The thermal behavior of the sample is investigated with the following temperature profile: the sample is quickly heated to 230 ° C and maintained isothermal for 3 minutes to remove any previous thermal history. The sample is then cooled to -90 ° C at a cooling rate of 10 ° C / min and held at -90 ° C for 3 minutes. The sample is then heated to 230 ° C at a heating rate of 10 ° C / min. The cooling curves and the second heating curve are recorded.

High Temperature Liquid Chromatography (HTLC)

[0092] HTLC is conducted according to the methods described in the publication of American patent application No. 2010-0093964 and American patent application No. 12/643111, filed on December 21, 2009, both of which are incorporated herein by reference. The samples are analyzed using the methodology described below.

[0093] A SEC high temperature GPCV2000 chromatograph from Waters has been reconfigured to assemble the HT-2DLC instrumentation. Two LC-20AD Shimadzu pumps were connected to the injection valve in GPCV2000 through a binary mixer. The first dimension HPLC column (D1) was connected between the injector and the 10-port switching valve (Valco Inc.). The second dimension SEC column (D2) was connected between the 10-port valve and the LS (Varian Inc.), IR (concentration and composition), RI (refractive index) and IR (intrinsic viscosity) detectors. IR and IV were detectors built into GPCV2000. The IR5 detector was supplied by PolymerChar, Valencia, Spain.

[0094] Columns: Column D1 was a high temperature Hypercarb graphite column (2.1 x 100 mm) purchased from Thermo Scientific. Column D2 was a PLRapid-H column purchased from Varian (10 x 100 mm).

[0095] Reagents: HPLC grade trichlorobenzene (TCB) was purchased from Fisher Scientific. 1-decanol and dean were purchased from Aldrich. 2,6-di-ter-butyl-4-methylphenol (Ionol) was also purchased from Aldrich.

[0096] Sample Preparation: 0.01 - 0.15 g of polyolefin sample was placed in a 10 ml self-sampling bottle from Waters. 7 ml of 1-decanol or decane with 200 ppm Ionol were added to the flask later. After spraying the sample vial with helium for about 1 min, the vial was placed on a heated shaker with a temperature set at 160 ° C. Dissolution was carried out by shaking the flask at temperature for 2 hours. The vial was then transferred to the automatic sampler for injection. Note that the actual volume of the solution was greater than 7 mL due to the thermal expansion of the solvent.

[0097] HT-2DLC: The D1 flow rate was 0.01 ml / min. The composition of the mobile phase was 100% of the weak eluent (1-decanol or decane) in the first 10 minutes of the operation. The composition was then increased to 60% of the strong eluent (TCB) in 489 min. The data were collected for 489 min while obtaining a raw data chromatogram. The 10-port valve switched every three minutes, producing 489/3 = 163 SEC chromatograms. A post-operation gradient was used after the data acquisition time of 489 min to clean and balance the column for the next operation: Cleaning step: 1. 490 min: flow = 0.01 min; // Keep the flow rate constant at 0.01 mL / min from 0 - 490 min. 2. 491 min: flow = 0.20 min; // Increase the flow rate to 0.20 mL / min. 3. 492 min:% B = 100; // Increase the composition of the mobile phase to 100% TCB 4. 502 min:% B = 100; // Wash the column using 2 ml of TCB.

Balance step:

[0098] 5. 503 min; % B = 0; // Change the mobile phase composition to 100% 1-decanol or decane

[0099] 6. 513 min:% B = 0; // Balance the column using 2 ml of weak eluent

[0100] 7. 514 min: flow = 0.2 ml / min; // maintain a constant flow of 0.2 mL / min from 491 - 514 min

[0101] 8. 515 min: flow = 0.01 ml / min; // reduce the flow rate to 0.01 mL / min.

[0102] After step 8, the flow rate and the mobile phase composition had the same initial conditions as the operating gradient.

[0103] The flow rate D2 was 2.51 ml / min. Two 60 μL loops were installed on the 10-port switching valve. 30 μL of column D1 eluent was loaded onto the SEC column with each switching of the valve.

[0104] The IR, LS15 (15 ° light scattering signal), LS90 (90 ° C light scattering) and IR (intrinsic viscosity) signals were collected by EZChrom via an analog-to-digital conversion box. digital SS420X. The chromatograms were exported in ASCII format and imported into MATLAB software for data reduction. An appropriate calibration curve of polymeric composition and polymer retention volume of a similar nature to that of the CAOB and CEB polymers under analysis was used. The calibration polymers must be narrow in composition (both molecular weight and chemical composition) and cover a reasonable molecular weight range to include the composition of interest during the analysis. The analysis of the raw (basic) data was calculated as described below, the first dimension HPLC chromatogram being reconstructed by plotting the IR signal of each cut (from the total cut SEC SEC chromatogram) as a function of the elution volume. The volume of elution IR vs. D1 was normalized by the total IR signal to obtain the weight vs. weight plot. elution volume D1. The methyl IR / measurement ratio was obtained from the reconstructed IR measurement and from the methyl IR chromatograms. The ratio was converted to composition using a calibration curve of% by weight of PP (through NMR) vs. methyl / measure obtained from the SEC experiments. The MW was obtained from the reconstructed IR measurement and from LS chromatograms. The ratio was converted to MW after calibration of both IR and LS detectors using a PE standard.

13C Nuclear Magnetic Resonance (NMR) Sample Preparation

[0105] Samples were prepared by adding approximately 2.7 g of a 50/50 mixture of tetrachloroethane-d2 / orthodichlorobenzene which is 0.025 M in chromium acetylacetonate (relaxation agent) to 0.21 g of sample in a tube 10 mm NMR. The samples are dissolved and homogenized by heating the tube and its contents to 150 ° C. Data Acquisition Parameters

[0106] Data are collected using a 400 MHz Bruker spectrometer equipped with a DUL Bruker Dual high temperature CryoProbre. Data is acquired using 320 transients per data file, a 7.3 sec pulse repetition delay (6 sec delay + 1.3 sec acquisition time), 90 degree turn angles, and discontinuous decoupling reverse with a sample temperature of 125 ° C. All measurements are made on samples without rotation in closed mode. The samples are homogenized immediately before insertion in the heated NMR sample changer (130 ° C) and allowed to thermally equilibrate in the probe for 15 minutes before data acquisition.

Gel permeation chromatography (GPC)

[0107] The gel permeation chromatographic system consists of an instrument model PL-210 or model PL-220 from Polymer Laboratories. The column and carousel compartments are operated at 140 ° C. Three 10 micron Mixed-B columns from Polymer Laboratories are used. The solvent is 1,2,4-trichlorobenzene. The samples are prepared at a concentration of 0.1 gram of polymer in 50 milliliters of solvent containing 200 ppm of butylated hydroxytoluene (BHT). The samples are prepared by gently shaking for 2 hours at 160 ° C. The injection volume used is 100 microliters and the flow rate is 1.0 ml / minute.

[0108] The calibration of the GPC column set is conducted with 21 polystyrene standards with narrow molecular weight distribution with molecular weights ranging from 580 to 8,400,000, arranged in 6 "cocktail" mixtures with at least a decade of separations between individual molecular weights. The standards are purchased from Polymer Laboratories (Shropshire, UK). Polystyrene standards are prepared at 0.025 grams in 50 milliliters of solvent for molecular weights equal to or greater than 1,000,000 and 0.05 grams in 50 milliliters of solvent for molecular weights less than 1,000,000. The polystyrene standards are dissolved at 80 ° C with slight agitation for 30 minutes. Mixtures of narrow standards are operated first and in decreasing order of the highest molecular weight component to minimize degradation. The peak molecular weights of polystyrene standard are converted to molecular weights of polyethylene using the following Equation (as described in Williams and Ward, J. Polym. Sci. Polym. Let., 6, 621 (1968)): Mpolethylene = 0.645 ( Mpoliesti reno).

[0109] Calculations of equivalent molecular weight of polypropylene are performed using version 3.0 of TriSEC Viscotek software.

Rapid Fractionation by Elution and Temperature Rise (F-TREF)

[0110] In the F-TREF analysis, the composition to be analyzed is dissolved in ortho-chlorobenzene and allowed to crystallize in a column containing an inert support (stainless steel sphere), slowly reducing the temperature to 30 ° C (at a preferred 0.4 ° C / min). The column is equipped with an infrared detector. An F-TREF chromatogram curve is then generated by eluting the crystallized polymer sample from the column by slowly increasing the temperature of the elution solvent (o-dichlorobenzene) from 30 to 140 ° C (at a preferred rate of 1.5 ° C / min).

Dynamic Mechanical Spectroscopy (DMS)

[0111] Dynamic mechanical measurements (loss and storage modules vs. temperature) are measured on a TA Instruments ARES. Dynamic module measurements are carried out under torsion on a solid bar 2 mm thick (approx.) 5 mm wide and 10 mm long (approx.). The data are recorded at a constant frequency of 10 rad / s and at a heating / cooling rate of 5 ° C / min. Temperature scans are performed from -50 to 190 ° C to 5 ° C / min. Transmission Electron Microscopy (TEM)

[0112] Polymeric films are prepared by compression molding followed by rapid cooling. The polymer is pre-melted at 190 ° C for 1 minutes at 6.9 MPa (1000 psi) and then pressed for 2 minutes at 34.5 MPa (5000 psi) and then quickly cooled between chilled plates (15-20 ° C) ) for 2 minutes.

[0113] Compression-molded films are trimmed so that sections can be collected close to the film core. The trimmed samples are cryopolished before staining by removing the sections of the blocks at -60 ° C to avoid contamination of the elastomeric phases. The cryopolished blocks are stained with the vapor phase of a 2% aqueous ruthenium tetraoxide solution for 3 hours at room temperature. The dye solution is prepared by weighing 0.2 g of ruthenium (III) chloride hydrate (RuCl3 x H2O) in a glass bottle with a screw cap and adding 10 ml of 5.25% aqueous sodium hypochlorite to the pitcher. The samples are placed in a glass jar using a glass slide with double-sided tape. The slide is placed in the flask to suspend the blocks approximately 1 inch above the dye solution. Sections approximately 90 nanometers thick are collected at room temperature using a diamond knife on a Leica EM UC6 microtome and placed in virgin 600 mesh TEM networks for observation.

Image Collection

[0114] TEM images are collected in a JEOL JEM-1230 operated at an acceleration voltage of 100 kV and collected by Gatan-791 and 794 digital cameras.

Cast Resistance

[0115] The compounds were measured for melt strength by Rheotens apparatus at 190 ° C and through dynamic EVF using ARES melt rheometer.

[0116] Melt strength (MS), as used here, is the maximum tensile force measured in a molten filament of an extruded polymer melt in a capillary rheometer matrix at a constant shear rate of 33 reciprocal seconds (sec-1) while the filament is being stretched by a pair of pressure cylinders that accelerate the filament at a rate of 0.24 centimeters per second per second (cm / sec2) from an initial speed of 1 cm / sec. The molten filament is preferably generated by heating 10 grams (g) of a polymer that is loaded into an Instron capillary rheometer barrel, balancing the polymer at 190 ° C for five minutes and then extruding the polymer at a speed of piston of 2.54 cm / minute (cm / min) through a capillary matrix with 0.21 cm in diameter and 4.19 cm in length. The tensile force is preferably measured with a Goettfert Rheotens installed in such a way that the pressure cylinders are 10 cm directly below a point at which the filament ejects from the capillary matrix.

Viscosity

[0117] Extensional viscosity measurements were performed using an ARES rheometer (TA Instruments) with an ARES-EVF accessory. Compression-molded samples are measured and have a dimension of 10 mm in width and between 0.3 to 1 mm in thickness. The test temperature is 190 ° C and the applied strain rate is 0.1%. The samples are mounted between the drum holders and the temperature stabilized for about three minutes. The measured torque is converted into extensional stress which is divided by the applied strain rate to obtain unaxial extensional or extensional viscosity. The solid density was 0.90 g / cm3 and the melt density was 0.78 g / cm3. Determination of the Composite Index in Crystalline Block (CBCI)

[0118] Because the compositions of these block copolymers have a CAOP and CAOB composed of crystalline polypropylene and a CEP and CEP composed of crystalline polyethylene, they cannot be fractionated by conventional means. Techniques based on solvent or temperature fractionation, for example, using xylene fractionation, solvent / non-solvent separation, fractionation by elution and temperature rise, or fractionation by elution and crystallization are not able to dissolve the block copolymer since the CEB and CAOB co-crystallize with CEP and CAOP, respectively. However, the use of a method such as high temperature liquid chromatography that separates polymer chains using a combination of a mixed solvent / non-solvent and a graphitic column, crystalline polymer species such as polypropylene and polyethylene can be separated from each other and the block copolymer.

[0119] For example, the Crystalline Block Composite examples, as described below, show a polypropylene fraction and a polyethylene fraction when separated by high temperature liquid chromatography (see Figure 1). The analysis shows that the amount of PP isolated is less than if the polymer were a simple mixture of homopolymer iPP (in this example, CAOP) and polyethylene (in this example, CEP). Consequently, the polyethylene fraction contains an appreciable amount of propylene that would not otherwise be present if the polymer were simply a mixture of iPP and polyethylene. To account for this "extra propylene", a mass balance calculation can be conducted to determine a crystalline composite composite index of the amount of the polypropylene and polyethylene fractions and the percentage by weight of propylene present in each of the fractions that are separated by HTLC. The polymers contained in the crystalline block composite include iPP-PE, unbound iPP, and unbound PE diblock, where the individual components of PP or PE may contain a minimum amount of ethylene or propylene, respectively. Composition of the Crystalline Block Composite

[0120] A sum of the% by weight of propylene of each component in the polymer, according to equation 1 results in the percentage by weight of global propylene (of the total polymer). This mass balance equation can be used to quantify the amount of iPP and PE present in the diblock copolymer. This mass balance equation can also be used to quantify the amount of iPP and PE in a binary mixture or extended to a ternary or n-component mixture. For CBCs, the total amount of iPP or PE is contained in the blocks present in the iPP and PP polymers in diblock and not bonded. % by weight of C3global = wPP (% by weight C3pp) + wPE (% by weight C3PE) Equation 1 where: Wpp = fraction by weight of PP in polymer WPE = fraction by weight of PE in polymer% weight C3PP = percentage by weight of propylene in PP component or block% weight C3PE = percentage by weight of propylene in PE component or block

[0121] Note that the overall weight percentage of propylene (C3) is preferably measured by NMR C13 or some other composition measurement that represents the total amount of C3 present in the total polymer. The% by weight of propylene in the iPP block (% by weight C3PP) is set to 100 or if otherwise known from its melting point by DSC, NMR measurement or other form of composition determination, this value can be entered in your place. Similarly, the% by weight of propylene in the PE block (% by weight C3PE) is set to 100 or if otherwise known from its melting point by DSC, NMR measurement or other form of composition determination, this value can be inserted instead. Calculation of the ratio of PP to PE in the crystalline block composite

onde: WPP = fração em peso de PP presente no polímero total % peso C3PP= porcentagem em peso de propileno em componente ou bloco de PP % peso C3PE = porcentagem em peso de propileno em componente ou bloco de PE Determinação da quantidade de Dibloco no Compósito em Bloco Cristalino[0122] Based on equation 1, the global weight fraction of PP present in the polymer can be calculated using Equation 2 of the total C3 mass balance measured in the polymer. Alternatively, it can also be determined from a mass balance of monomer and comonomer consumption during polymerization. Generally, it represents the amount of PP and PE present in the polymer, regardless of whether it is present in unbound components or in the diblock copolymer. For a conventional mixture, the weight fraction of PP and the weight fraction of PE corresponds to the individual amount of PP and PE polymer present. For the crystalline block composite, it is assumed that the ratio of the weight fraction of PP to PE also corresponds to the average block ratio between PP and PE present in this statistical block copolymer.

where: WPP = fraction by weight of PP present in the total polymer% weight C3PP = percentage by weight of propylene in a component or block of PP% weight C3PE = percentage by weight of propylene in a component or block of PE Determination of the amount of Diblock in the Composite in Cristalino Block

onde: Wpp isolado = fração em peso de PP isolado de HTLC Wfração-PE = fração em peso de PE separado de HTLC, contendo o dibloco e o PE não ligado % peso C3PP = % peso de propileno no PP; que é também a mesma quantidade de propileno presente bloco de PP e no PP não ligado % peso C3fração-PE = % peso de propileno na fração-PE que foi separada através de HTLC % peso C3-global = % peso global no polímero total[0123] When applying equations 3 to 5, the amount of the isolated PP that is measured through HTLC analysis, is used to determine the amount of polypropylene present in the diblock copolymer. The amount isolated or separated first in the HTLC analysis represents the "unbound PP" and its composition represents the hard block of PP present in the diblock copolymer. When replacing the total weight% of C3 of the total polymer on the left side of equation 3, and the weight fraction of PP (isolated from HTLC) and the weight fraction of PE (separated via HTLC) from the right side of equation 3 , the weight% of C3 in the PE fraction can be calculated using equations 4 and 5. The PE fraction is described as the fraction separated from unbound PP and contains the diblock and unbound PE. It is assumed that the composition of the isolated PP is equal to the% by weight of propylene in the iPP block as previously described.

where: Isolated wpp = fraction by weight of PP isolated from HTLC W fraction-PE = fraction by weight of PE separated from HTLC, containing the diblock and unbound PE% weight C3PP =% weight of propylene in PP; which is also the same amount of propylene present in the PP block and in the unbound PP% weight C3-fraction-PE =% weight of propylene in the PE-fraction that was separated by HTLC% weight C3-global =% weight global in the total polymer

[0124] The amount of% by weight of C3 in the polyethylene fraction of HTLC represents the amount of propylene present in the block copolymer fraction which is above the amount present in "unbound polyethylene".

[0125] To account for the "additional" propylene present in the polyethylene fraction, the only way to have the PP present in this fraction is for the PP polymer chain to be connected to a PE polymer chain (or even if it has been isolated with the fraction of PP separated by HTLC). Thus, the PP block remains adsorbed with the PE block until the PE fraction is separated.

onde: % peso C3fração-PE = % peso propileno na fração-PE que foi separada por HTLC (Equação 4) % peso C3PP = % peso de propileno no componente ou bloco PP (anteriormente definido) % peso C3PE = % peso de propileno no componente ou bloco PE (anteriormente definido) Wdibloco-PP = fração em peso de PP no dibloco separado com fração PE através de HTLC[0126] The amount of PP present in the diblock is calculated using Equation 6.

where:% weight C3 fraction-PE =% weight propylene in the PE-fraction that was separated by HTLC (Equation 4)% weight C3PP =% weight of propylene in the PP component or block (previously defined)% weight C3PE =% weight of propylene in component or PE block (previously defined) Wdibloco-PP = weight fraction of PP in the separate diblock with PE fraction via HTLC

[0127] The amount of diblock present in that PE fraction can be determined assuming that the ratio of PP block to PE block is equal to the overall ratio of PP to PE present in the total polymer. For example, if the overall ratio of PP to PE is 1: 1 in the total polymer, then it is assumed that the ratio of PP to PE in the diblock is also 1: 1. Thus, the weight fraction of diblock present in the PE fraction would be the weight fraction of PP in the diblock (Wdibloco pp) multiplied by two. Another way of calculation is to divide the weight fraction of PP in the diblock (Wdibloco-PP) by the weight fraction of PP in the total polymer (equation 2).

[0128] To further determine the amount of diblock present in the total polymer, the estimated amount of diblock in the PE fraction is multiplied by the weight fraction of the measured HTLC PE fraction.

onde: Wdibloco-PP = fração em peso de PP no dibloco separado com a fração-PE por HTLC (Equação 6) WPP = fração em peso de PP no polímero Wfração-PE = fração em peso de PE separado de HTLC, contendo o dibloco e o PE não ligado (Equação 5).[0129] To evaluate the composite index in crystalline block, the amount of copolymer in diblock is determined by equation 7. To evaluate CBCI, the fraction by weight of diblock in the PE fraction calculated using equation 6 is divided by the fraction in overall weight of PP (calculated in equation 2) and then multiplied by the weight fraction of the PE fraction. The CBCI value can vary from 0 to 1, with 1 being equal to 100% diblock and zero being equal to a material such as a traditional mixture or random copolymer.

where: Wdibloco-PP = fraction by weight of PP in the separated diblock with the PE fraction by HTLC (Equation 6) WPP = fraction by weight of PP in the polymer W fraction-PE = fraction by weight of PE separated from HTLC, containing the diblock and unbound PE (Equation 5).

[0130] CBC1 contains a total of 62.5% by weight of C3 and is prepared under conditions to produce a PE polymer with 10% by weight of C3 and an iPP polymer containing 97.5% by weight of C3, as weight fractions of PE and PP being 0.400 and 0.600, respectively (calculated using Equation 2). Since the percentage of PE is 40.0% by weight and iPP is 60.0% by weight, the relative PE: PP block ratio is expressed as 1: 1.5.

[0131] Thus, if one skilled in the art conducts an HTLC separation of the polymer and isolates 28% by weight of the PP fraction and 72% by weight of the PE fraction, we would arrive at an unexpected result, which would lead to the conclusion of that a fraction of diblock copolymer was present. If the C3 content of the PE fraction (% weight C3fraction-PE) is subsequently calculated as 48.9% by weight of C3 based on equations 4 and 5, the PE fraction containing the additional propylene will have a weight fraction of 0.556% PE polymer and a weight fraction of 0.444 PP polymer (WPP-diblock, calculated using Equation 6).

[0132] Since the PE fraction contains a weight fraction of 0.444 PP, it should be linked to an additional 0.293 weight fraction of PE polymer based on the iPP-PE block ratio of 1.5: 1. Thus, the weight fraction of diblock present in the PE fraction is 0.741; another calculation of the weight fraction of diblock present in the total polymer is 0.533. For the total polymer, the composition is described as 53.3% by weight of iPP-PE diblock, 28% by weight of PP polymer, and 18.7% by weight of PE polymer. The crystalline block composite index (CBCI) is the estimated weight fraction of diblock present in the total polymer. For the example described above, the CBCI for the crystalline block composite is 0.533.

Observe que o cálculo de CBCI aplica-se somente aos CBCs e a misturas.[0133] Example CBCI calculations are shown in Table 1 for the CBCI Example. Also shown in Table 1 are the calculations for an equivalent mixture of polymers with the same CBCI composition consisting of a CAOP (random iPP) and CEP (random PE). Note that the calculation of CBC1 applies only to CBCs and mixtures. For illustrative purposes, the calculation of CBCI for the random polymer of individual iPP or PE results in a CBCI of zero, since it is not possible to have PP in the PE fraction. Therefore, for conventional purposes, the CBCI value of an individual random copolymer is assigned zero based on the intention of the method.

Note that the CBCI calculation applies only to CBCs and mixtures.

[0135] The Crystalline Block Composite Index (CBCI) provides an assessment of the amount of block copolymer in the crystalline block composite under the hypothesis that the ratio of CEB to CAOB in the diblock is equal to the ratio of crystalline ethylene to alpha- crystalline olefin in the global crystalline block composite.

[0136] This hypothesis is valid for these statistical block olefinic copolymers based on the understanding of individual catalytic kinetics and the polymerization mechanism for the formation of diblocks via chain transfer catalysis as described in the report.

[0137] The CBCI calculation is based on the analytical observation that the amount of free CAOP is less than the total amount of CAOP that was produced in the polymerization. The rest of the CAOP is linked to CEB to form the diblock copolymer. Because the fraction of PE separated through HTLC contains both CEP and diblock polymer, the observed amount of propylene for this fraction is above that of CEP. This difference can be used to calculate the CBCI.

[0138] Figure 2 shows a general graphical representation of the ratio of fraction by weight of CAO in the polymer to CBCI.

[0139] Based solely on analytical observations without prior knowledge of polymerization statistics, the minimum and maximum amounts of block copolymer present in a polymer can be calculated, thus distinguishing a crystalline block composite from a simple copolymer or copolymer mixture .

[0140] The superior bond in the amount of block copolymer present in a crystalline block composite, wDBmax, is obtained by subtracting the fraction of unbound PP measured through HTLC from one as in Equation 8. This maximum value assumes that the fraction HTLC PE is entirely diblock and that all crystalline ethylene is bound to the crystalline PP without unbound PE. The only material in the CBC that is not a block is that portion of PP separated via HTLC.

[0141] The lower bond in the amount of diblock copolymer present in a crystalline block composite, WDBmin, corresponds to the situation in which little or no PP is linked to PP. This lower limit is obtained by subtracting the amount of unbound PP as measured by HTLC from the total amount of PP in the sample, as shown in Equation 9.

[0142] In addition, the crystalline block composite index falls between these two values: WDB min <CBCI <WDBMax. Table 2 shows the connections in the diblock content for the examples. Because each of these examples contains a lower bond in the diblock weight fraction, WDBMin, which is significantly greater than zero, all of these samples are crystalline block composites.

[0143] Based on the polymerization mechanism for the production of crystalline block composites, CBCI represents the best estimate of the real fraction of diblock copolymer in the composite. For unknown polymer samples, WDBmin can be used to determine whether a material is a crystalline block composite. Consider applying this analysis to homopolymers, copolymers or mixtures. For a physical mixture of PE and PP, the total weight fraction of PP must equal the weight percentage of PP of HTLC and the lower bond in the diblock content, Equation 9, is zero. If this analysis is applied to a PP sample that does not contain PE, both the weight fraction of PP and the amount of PP obtained from HTLC are 100% and again the lower bond in the diblock content, Equation 9, is zero. Finally, if this analysis is applied to a PE sample that does not contain PP, then both the weight fraction of PP and the weight fraction of PP recovered via HTLC are zero and the bottom link in the diblock, Equation 9, is zero. Because the lower bond in the diblock content is not greater than zero in any of these three cases, these materials are not crystalline block composites.

EXAMPLES Examples General Crystalline Block Composite

[0144] Catalyst-1 ([[rel-2 ', 2 "' - [(1R, 2R) -1,2-cyclohexanediilbis (methylenoxy-KO)] bis [3- (9H-carbazol-9-yl) - 5- methyl [1,1'-biphenyl] -2-olate-KO]] (2 -)] dimethyl-hafnium) and cocatalyst-1, a mixture of salts of tetracis (pentafluorophenyl) methyldi borate (C14-18 alkyl ) ammonium, prepared by the reaction of a long chain trialkylamine (ArmeenTMM2HT, from Akzo Nobel, Inc.), HCl and Li [B (C6F5) 4], substantially as described in USP 5,919,9883, Ex.2, are purchased from Boulder Scientific and used without further purification.

[0145] CSA-1 (diethylzinc or TEN) and cocatalyst-2 (modified methylalumoxane (MMAO)) were purchased from Akzo Nobel and used without further purification. The solvent for polymerization reactions is a hydrocarbon mixture (ISOPAR®E) obtained from ExxonMobil Chemical Company and purified through 13-X molecular sieve beds prior to use.

[0146] The crystalline block composite of the Examples of the present invention are designated as CBC1, CBC2 and CBC3.

[0147] CBC1, CBC2 and CBC3 are prepared using two continuous agitated tank reactors (CSTR) connected in series. Each reactor is hydraulically filled and adjusted to operate in steady state conditions. Monomers, solvent, catalyst-1, cocatalyst-1 and CSA-1 are drained to the first reactor according to the process conditions defined in Table 3. The contents of the first reactor, as described in Table 1, are drained to a second series reactor. Additional catalyst-1 and cocatalyst -1 are added to the second reactor, as well as a small amount of MMAO as a sweeper. The hydrogen flow in the first reactor for CBC1 is 12 sccm and for CBC2 and CBC3 it is 10 sccm. The DEZ solution concentration is maintained at 30,000 ppm and added to the first reactor only. The concentration of cocatalyst-1 in the first reactor for CBC1 is 149 ppm and for CBC2 and CBC3 it is 50 ppm. The concentration of Cocatalyst-2 in the first reactor for CBC1 is 1993 ppm and for CBC2 and CBC3 it is 1500 ppm.

[0148] Table 4 shows the analytical characteristics of CBC1, CBC2 and CBC3. Table 4 - Physical Properties of Block Composite

[0149] Table 5 shows the ratio of iPP to PE in CBC1, CBC2 and CBC3, as well as the estimated crystalline block composite index.

[0150] Figure 3 shows the DSC profile for CBC1. The DSC profile shows a melting peak at 127 ° C representing CAOP and CAOB and 110 ° C corresponding to CEP and CEB. The melting enthalpy observed was 96 J / g and the glass transition temperatures were observed at 0 and -24 ° C. The crystallization temperature was measured at 90 ° C. Surprisingly, the temperature of crystallization of CBC1 is closer to the temperature of crystallization of CEP than of CAOP.

[0151] Figure 1 shows the TREF analysis of CBC1. The TREF elution profile shows that CBC1 is highly crystalline and, unlike the DSC fusion profile, shows little or no separation of CEP and CAOP or the block copolymer. Only 2.4% purging weight was measured which also indicates the very high crystallinity of components in CBC1.

[0152] Figure 4 shows the HTLC analysis of CBC1. The elution profile of CBC1 through HTLC showed that 28% by weight of an early elution peak between 1-2 ml and 72% by weight of a later elution peak between 3-6 ml were eluted. From the measurement of concentration and composition, it was determined that the early elution peak was isolated PP which is CAOP and which represents CAOB. This is shown by the composition profile of the percentage by weight of C3 present. The second peak and the posterior elution peak are rich in C2 and show a gradient of C3. It can be interpreted that this peak is the PE phase and that it contains the block copolymer and the CEP. The composition gradient shows that the block copolymer is eluted first and the CEP is eluted last.

[0153] Figure 5 is a TEM micrograph showing the morphology of CBC1 at a resolution of 2 μm. Figure 6 shows the morphology at 0.5 μm and Figure 7 shows it at 100 nm. Based on the applied dye, the darkest domains are PE and the lightest domains are PP. The very small PE domain size of this composition strongly suggests the presence of high levels of block copolymers that acted to make the PP and PE phases compatible. The spherical and nanoscale nature indicated that the block copolymer was effective in reducing PE domains. Polymer / standard polymer mixtures of polypropylene and polyethylene exhibit coarse and phase-separated morphologies with an order of magnitude greater than the domain size. Mixtures of Polypropylene and Polyethylene with CBC1

[0154] Polypropylene H 110-02N (PP) (The Dow Chemical Company) (0.900 g / cm3, 2MFR) was used for the polypropylene component in the mixtures.

[0155] 662I Low Density Polyethylene (LDPE1) (The Dow Chemical Company) (0.919 g / cm3, 0.47 MFR) was used as the polyethylene component in the mixtures.

[0156] 640I Low Density Polyethylene (LDPE2) (The Dow Chemical Company) (0.920 g / cm3, 2.0 MFR) was used as a polyethylene component in the mixtures.

[0157] The CBC1 crystalline block composite is added at the level of 5 and 10% by weight based on the total weight of the polymer.

[0158] The mixtures were prepared in a Haake batch mixer using a 200 gram container. The blends / mixtures were mixed at 190 ° C at 50 rpm for fifteen minutes. During this period, the melting torque was monitored to ensure that it reached a constant state after melting the components.

• Medida como diâmetros circulares equivalentes em μm.[0159] Table 6 shows the combined formulas while Table 7 shows the physical properties of the blends. Table 8 shows the image analysis for Mixture B and Mixture 4.

• Measured as equivalent circular diameters in μm.

[0160] Figure 8 shows the morphology of Mixture B, 80% by weight of PP and 20% by weight of LDPE1 compared to Mixture 4, 70% by weight of PP and 20% by weight of LDPE1 compatible with 10% by weight of CBC1. LDPE1 is shown as the darkest domain areas. The reduction in the domain sizes of LDPE1 is surprising and dramatic. Domain sizes were reduced from 0.88 μm to 0.14 μm. As shown, the LDPE domain sizes shown for the Mixture 4 example are less than 210 nm with an equivalent average diameter of 140 nm. In comparison to Mixture B, a wide particle size distribution was observed in the LDPE domains in the range of 0.2 to 2.25 μm, with an equivalent average diameter of 0.88 μm.

[0161] Figure 9 compares the melt strength of comparative Mix A and Mixtures 1 and 3 compatible with 5 and 10% by weight of CBC1 addition. Surprisingly, the compatible mixtures exhibit 250-300% improvement in melt strength.

[0162] Figure 10 compares the melt strength of comparative Mix B and Mixtures 2 and 4 compatible with 5 and 10% CBC1 addition. Surprisingly, these compatible mixtures also exhibit 250-300% improvement in melt strength.

[0163] Figure 11 compares the extensional viscosity at 190 ° C measured using EVF ARES. The observed extensional viscosity increases with the increasing level of LDPE1 in the mixture. It is shown that the compatible mixture, Mixture 6, containing 45% PP, 45% LDPE1, and 10% CBC1 approximates the extensional viscosity behavior of LDPE 170A (The Dow Chemical Company) (0.923 g / cm3, 0, 6 MI). A 10% compatibilized mixture containing 22.5% PP H110N, 67.5% LDPE 662I, and 10% CBC1 comes close to the extensional viscosity behavior of Profax PF814 (Basell Polyolefins) (0.902 g / cm3, 3.0 MFR ).

[0164] Figure 12 compares the melt strength of Mixture B and Mixtures 4, 6 and 7 compatible with 10% addition of CBC1. As the LDPE1 level is increased to 67% in the mixture, the melt strength can be increased to 20 cN at 100 mm / s @ 190 ° C. A corresponding increase in melt strength is observed with the increasing level of LDPE1 in the mixture. Plastomer / elastomer mixtures based on polyethylene and propylene

[0165] 662I Low Density Polyethylene (LDPE1) (The Dow Chemical Company) (0.919 g / cm3, 0.47 MFR) was used as the polyethylene component in the mixtures.

[0166] VERSIFY 2200 (PBP) (The Dow Chemical Company) (0.876 g / cm3, 2.0 MFR) was used as the propylene-based plastomer in the mixtures.

[0167] VERSIFY 2400 (PBE) (The Dow Chemical Company) (0.859 g / cm3, 2.0 MFR) was used as the propylene-based elastomer in the mixtures.

[0168] The CBC1 crystalline block composite is added at the level of 5 and 10% by weight based on the total polymer weight.

[0169] The mixtures were prepared in a Haake batch mixer using a 200 gram container. The blends were mixed at 190 ° C at 50 rpm for fifteen minutes. During this period, the melting torque was monitored to ensure that it reached a constant state after melting the components. Refer to Table 9 for the combined formulas. Table 10 shows the physical properties of the mixtures. Table 9 - Compositions, parts by weight for plastomer and propylene-based elastomer

[0170] Figure 13 compares the melt strength of Mixture C and Mixtures 8 and 10 compatible with 10% by weight of addition CBC1. Mixture 10 containing 45 wt% LDPE1 and 45 wt% PBP and 10 wt% CBC1 showed the highest melt strength at 100 mm / s. When comparing Mixture 8 with Mixture C, it appears that the melt strength of the compatible mixture is slightly improved over Mixture C.

[0171] Figure 14 compares the melt strength of Mixture D and Mixtures 9 and 11 compatible with 10% by weight of CBC1 addition. Mixture 11 containing 45 wt% LDPE1 and 45 wt% PBE and 10 wt% CBC1 showed the highest melt strength at 100 mm / s. When comparing Mixture 9 and Mixture B, the melt strength of the compatible mixture is slightly improved over Mixture D.

[0172] Although the present invention has been described with respect to a limited number of embodiments, the specific characteristics of an embodiment should not be attributed to other embodiments of the invention. No embodiment, by itself, represents all aspects of the invention. In some embodiments, the compositions or methods can include numerous compounds or steps not mentioned in the present invention. In other embodiments, the compositions or methods do not include, or are substantially free from, any compounds or steps not mentioned in the present invention. There are variations and modifications to the described embodiments. Finally, any number described here should be interpreted as meaning approximate, regardless of whether the word "about" or "approximately" is used to describe the number. The attached claims are intended to cover all such modifications and variations, included in the scope of the invention.

Claims (5)

1. Composition, characterized by the fact that it comprises: A) a polypropylene, a polypropylene copolymer or a crystalline polyalphaolefin copolymer that has a first order transition or crystalline melting point as determined by exploratory differential calorimetry, selected from polybutylene and poly (4 - methylpentene), B) an LDPE having a density of 0.91 g / cm3 to 0.94 g / cm3, and C) at least one polymer compatibilizer being a crystalline block composite comprising: i) an ethylene-based polymer crystalline; D)) a crystalline alpha-olefin-based polymer; and E) i) a block copolymer comprising a crystalline ethylene block and a crystalline alpha-olefin block, the crystalline ethylene block being essentially the same composition as the crystalline ethylene-based polymer in the block composite, and the crystalline alpha-olefin block is essentially the same composition as the crystalline alpha-olefin-based polymer of the block composite, with component C) having a first order transition or crystalline melting point as determined by scanning calorimetry differential, with component C) present in an amount of 0.5% by weight to 15% by weight based on the total weight of the composition, and component C) having a Crystalline Block Composite Index greater than 0.0 to 1.0, the Crystalline Block Composite Index being determined using high temperature liquid chromatography on a first dimension HPLC column and a second dimension SEC column using 1-decanol o u dane with 200 ppm 2,6-di-tert-butyl-4-methylphenol. 2. Composition according to claim 1, characterized in that component A) is a propylene-based elastomer or a propylene-based plastomer. Composition according to either of claims 1 or 2, characterized in that component C) has a Crystalline Block Composite Index of 0.1 to 0.9. Composition according to any one of claims 1 to 3, characterized in that the melt strength of the composition at 100 mm / s and 190 ° C is at least 115% greater than that of the composition without component (C) , the melt strength of the composition being measured using a 190 ° C rheometer as mentioned in the description. Composition according to any one of claims 1 to 4, characterized in that the average particle diameter of the composition, as measured by TEM, is at least 50% smaller than that of the composition without component (C).

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